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RESEARCH ON MEMBRANE BIOREACTOR TREATING DOMESTIC WASTEWATER AND RELATED MECHANISMS
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作者 顾平 周丹 +1 位作者 杨造燕 刘锦霞 《Transactions of Tianjin University》 EI CAS 2001年第1期7-11,共5页
Experiments on treatment of domestic wastewater by membrane bioreactors were carried out.The results showed that this process could produce good quality effluent with low COD,turbidity and total count of bacteria.With... Experiments on treatment of domestic wastewater by membrane bioreactors were carried out.The results showed that this process could produce good quality effluent with low COD,turbidity and total count of bacteria.With intermittent operation and continuous aeration,the membrane flux was kept steady.The mechanisms of removing COD through membrane,the structure of membrane and filtration resistance were also discussed. 展开更多
关键词 wastewater treatment domestic wastewater membrane bioreactor electronic microscopic photograph filtration resistance
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Physical Modelling of the Drained Flow on a Suction Box of a Papermachine
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作者 Jean-Claude Roux Martine Rueff 《Journal of Chemistry and Chemical Engineering》 2011年第2期165-169,共5页
Suction boxes are used in the paper industry to simultaneously drain a pulp suspension and form a fibre mat (or filter cake). This research addresses the modelling of fibre deposition in the forming unit of an indus... Suction boxes are used in the paper industry to simultaneously drain a pulp suspension and form a fibre mat (or filter cake). This research addresses the modelling of fibre deposition in the forming unit of an industrial papermachine, assuming a filtration process, and that of the flowing suspension drained through the building fibre mat and the wire on a suction box. From experimental data of the cumulative drained V volume, per unit surface area, for two vacuum pressures △P and 6 dwell times t, an extension of the classical law (t/V) versus V is proposed, validated and applied. This relation enables determining the average specific filtration resistance of the fibre mat over the box and the mass of solids deposited before and over the suction box. The model obtained is as precise as 1% and can be used to limit and reduce the energy consumption of drainage vacuum assisted devices such as suction boxes in the forming unit of industrial papermachines. 展开更多
关键词 Papermachine suction box physical modelling specific filtration resistance fibre deposition "dead-end" filtration
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Settling and dewatering characteristics of granulated methane-oxidizing bacteria
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作者 Kwang Ho Ahn Kwang Soo Kim +3 位作者 Sung Won Kang Chul Yong Um Won Tae Lee Kwang Baik Ko 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2013年第2期280-286,共7页
We evaluated the settling ability and dewaterability of granulated methane-oxidizing bacteria (GMOB) after granulation using a continuous-flow reactor. A comparative analysis on settling and dewatering characteristi... We evaluated the settling ability and dewaterability of granulated methane-oxidizing bacteria (GMOB) after granulation using a continuous-flow reactor. A comparative analysis on settling and dewatering characteristics due to changes in sludge retention time (SRT, 10, 15 and 20 days) during cultivation of GMOB was conducted. In assessing dewaterability, the specific resistance to filtration (SRF) of activated sludge and GMOB was found to be 8.21×1013-2.38×1014 and 4.88 × 1012-1.98×1013 m/kg, respectively. It was confirmed that as SRT decreased, SRF of GMOB increased. In the case of bound extracellular polymeric substance (EPS), activated sludge registered 147.5 mg/g-VSS while GMOB exhibited 171-177.2 mg/g-VSS. In the case of extracellular polymeric substance soluble EPS in effluent, activated sludge measured 62 mg/L and GMOB had 17.4-21.4 mg/L. The particle size analysis showed that mean particle diameters of GMOB were 402, 369, and 350 μm, respectively, at SRTs of 20, 15 and 10 days. In addition, it was found that GMOB had a larger mean particle diameter and exhibited much better settleability and dewaterability than activated sludge did. 展开更多
关键词 methane-oxidizing bacteria dewaterability specific resistance to filtration extracellular polymeric substances
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